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CN110108444B - An experimental device for sulfur deposition in sulfur-bearing natural gas pipelines - Google Patents

An experimental device for sulfur deposition in sulfur-bearing natural gas pipelines Download PDF

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CN110108444B
CN110108444B CN201910349009.6A CN201910349009A CN110108444B CN 110108444 B CN110108444 B CN 110108444B CN 201910349009 A CN201910349009 A CN 201910349009A CN 110108444 B CN110108444 B CN 110108444B
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sulfur
pipeline
gas
control valve
pressure
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CN110108444A (en
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范开峰
李思
王卫强
张颜
吴玉国
于龙风
周海波
李嘉宁
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Liaoning Shihua University
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Abstract

本发明涉及一种含硫天然气管道硫沉积实验装置,包括储气系统、环道系统和溶硫剂加注系统,所述储气系统和溶硫剂加注系统安装在环道系统上。所述环道系统包括拆卸式管段,拆卸式管段为可拆卸结构方便实验,实验结束后可以通过固定装置进行固定,加热融化硫沉积物。本发明可以分析特定时间、温度、压力、流速、管壁表面粗糙度等变量对硫沉积规律的影响,同时可以研究不同类型溶硫剂对硫沉积物的清除效果,可以很好的模拟并分析真实高含硫天然气管线中的硫沉积规律。

Figure 201910349009

The invention relates to an experimental device for sulfur deposition in a sulfur-containing natural gas pipeline, comprising a gas storage system, a loop system and a sulfur-dissolved agent filling system, wherein the gas storage system and the dissolved-sulfur agent filling system are installed on the loop system. The loop system includes a detachable pipe section, and the detachable pipe section is of a detachable structure to facilitate experiments. After the experiment, it can be fixed by a fixing device, and the sulfur deposits can be heated and melted. The invention can analyze the influence of variables such as specific time, temperature, pressure, flow rate, and surface roughness of the pipe wall on the sulfur deposition law, and at the same time, it can study the removal effect of different types of sulfur-dissolving agents on sulfur deposits, and can simulate and analyze well Sulfur deposition in real high-sulfur natural gas pipelines.

Figure 201910349009

Description

一种含硫天然气管道硫沉积实验装置An experimental device for sulfur deposition in sulfur-bearing natural gas pipelines

技术领域technical field

本发明属于管输天然气技术领域,特别是涉及一种含硫天然气管道硫沉积实验装置。The invention belongs to the technical field of pipeline transportation of natural gas, in particular to an experimental device for sulfur deposition in a sulfur-containing natural gas pipeline.

背景技术Background technique

我国高含硫气田储量大、分布广,如元坝气田、普光气田等,其中,普光气田的H2S平均含量15.16%,含硫天然气开采过程中集输系统的硫沉积问题日益突出。高含硫天然气输送过程中受压力、温度、流速等因素的影响会出现析硫和硫沉积现象,在集输系统管壁上经常会发现淡黄色粉末状和黏稠状的硫沉积物,严重威胁管输系统安全。主要体现在以下几方面:(1)析出和沉积的硫组分容易堵塞管路上的仪表引压管、计量孔板等设备,造成测试结果失真,采集的数据不准确,存在巨大安全隐患。(2)管壁上发生硫沉积以后,会导致气体过流面积变小,使得管道压降增大和能耗增加,降低集输效率。(3)管壁上的硫沉积物会改变管壁表面的电场、磁场、温度场等环境,加速管壁腐蚀,威胁材料结构安全。High-sulfur gas fields in China have large reserves and wide distribution, such as Yuanba Gas Field and Puguang Gas Field. Among them, the average H 2 S content of Puguang Gas Field is 15.16%, and the problem of sulfur deposition in gathering and transportation systems during the extraction of sulfur-containing natural gas is becoming more and more prominent. During the transportation of high-sulfur natural gas, under the influence of pressure, temperature, flow rate and other factors, sulfur precipitation and sulfur deposition will occur. Light yellow powdery and viscous sulfur deposits are often found on the pipe wall of the gathering and transportation system, which is a serious threat. Pipeline system safety. It is mainly reflected in the following aspects: (1) The precipitated and deposited sulfur components are easy to block the instrument pressure pipes, metering orifice plates and other equipment on the pipeline, resulting in distorted test results, inaccurate data collected, and huge potential safety hazards. (2) After sulfur deposition occurs on the pipe wall, the gas flow area will become smaller, which will increase the pipeline pressure drop and energy consumption, and reduce the gathering and transportation efficiency. (3) The sulfur deposits on the pipe wall will change the electric field, magnetic field, temperature field and other environments on the pipe wall surface, accelerate the corrosion of the pipe wall, and threaten the safety of the material structure.

硫沉积的影响因素主要分为热力学和动力学两部分,包括气体温度、气体与管壁温差、流速、管壁粗糙度等。前期的一些研究结果表明:元素硫饱和溶解度随硫化氢含量的增加而增加,在组分一定的情况下,随压力、温度的升高而增大。且元素硫溶解度在50~80℃的范围内随温度升高增加幅度最快;在30℃以下元素硫溶解度随温度增加升幅不大。但可以测试和研究热力学和动力学因素对高含硫气田采出气硫沉积规律影响的实验装置并不多见,严重制约着硫沉积规律和特性的深入研究。The influencing factors of sulfur deposition are mainly divided into two parts: thermodynamics and kinetics, including gas temperature, temperature difference between gas and tube wall, flow rate, and tube wall roughness. Some previous research results show that the saturated solubility of elemental sulfur increases with the increase of hydrogen sulfide content, and increases with the increase of pressure and temperature under the condition of certain components. And the solubility of element sulfur in the range of 50-80 ℃ increases the fastest with the increase of temperature; below 30 ℃, the solubility of element sulfur increases little with the increase of temperature. However, there are few experimental devices that can test and study the effects of thermodynamic and kinetic factors on the sulfur deposition law in the produced gas from high-sulfur gas fields, which seriously restricts the in-depth study of the sulfur deposition law and characteristics.

发明内容SUMMARY OF THE INVENTION

为了解决上述存在的技术问题,本发明提供一种含硫天然气管道硫沉积实验装置,可以有效的研究热力学和动力学因素对硫沉积规律的影响机理,同时,可以评价和研究不同溶硫剂对硫沉积的消除情况。In order to solve the above existing technical problems, the present invention provides a sulfur deposition experimental device for a sulfur-containing natural gas pipeline, which can effectively study the influence mechanism of thermodynamic and kinetic factors on the sulfur deposition law, and at the same time, can evaluate and study the effect of different sulfur-dissolving agents on the sulfur deposition law. Elimination of sulfur deposits.

本发明采用的技术方案如下:The technical scheme adopted in the present invention is as follows:

一种含硫天然气管道硫沉积实验装置,包括储气系统、环道系统和溶硫剂加注系统,所述储气系统为高压气罐,所述环道系统包括环道管线,环道管线上连通高压气罐和拆卸式管段,高压气罐的一侧和拆卸式管段之间依次设有第一控制阀门、第一压力表、压缩机、第二压力表和溶硫剂加注系统,溶硫剂加注系统和环道管线之间设有第二控制阀门;所述拆卸式管段的两端分别设有控温水浴入口和控温水浴出口,控温水浴入口和控温水浴出口之间通过水管连通控温水浴;所述拆卸式管段和高压气罐的另一侧之间依次设有第一止回阀、质量流量计、第二止回阀和第五控制阀门;环道管线上在第一止回阀和第二止回阀的两端并联旁通管路,旁通管路和环道管线之间分别设有第三控制阀门和第四控制阀门。An experimental device for sulfur deposition in a sulfur-containing natural gas pipeline, comprising a gas storage system, a loop system and a sulfur-dissolving agent filling system, wherein the gas storage system is a high-pressure gas tank, and the loop system includes a loop pipeline and a loop pipeline. The upper part is connected with the high-pressure gas tank and the dismantling pipe section, and a first control valve, a first pressure gauge, a compressor, a second pressure gauge and a dissolved sulfur agent filling system are arranged between one side of the high-pressure gas tank and the dismantling pipe section. A second control valve is arranged between the sulfur-dissolving agent filling system and the loop pipeline; the two ends of the detachable pipe section are respectively provided with a temperature-controlled water bath inlet and a temperature-controlled water bath outlet, and the temperature-controlled water bath inlet and the temperature-controlled water bath outlet are arranged between the temperature-controlled water bath inlet and the temperature-controlled water bath outlet. A first check valve, a mass flow meter, a second check valve and a fifth control valve are arranged between the disassembled pipe section and the other side of the high-pressure gas tank in sequence; the loop pipeline A bypass pipeline is connected in parallel at both ends of the first check valve and the second check valve, and a third control valve and a fourth control valve are respectively arranged between the bypass pipeline and the loop pipeline.

本发明的有益效果:Beneficial effects of the present invention:

(1)可以模拟现场输气管道硫沉积环境,针对性的研究压力、气体温度、气体与管壁温差、气体流速、管壁粗糙度、管壁材质等变量和因素对硫沉积的影响规律;(1) It can simulate the sulfur deposition environment of on-site gas pipelines, and specifically study the influence of variables and factors such as pressure, gas temperature, temperature difference between gas and pipe wall, gas flow rate, pipe wall roughness, and pipe wall material on sulfur deposition;

(2)采用可拆卸结构的拆卸式管道作为实验管段,方便对沉积物称重和取样,为进一步分析沉积物特性提供便利,同时,可拆卸管段可以加工成不同管壁粗糙度和材料的替换管段,使得实验操作灵活、多变;(2) The detachable pipe with detachable structure is used as the experimental pipe section, which is convenient for weighing and sampling the sediment, and provides convenience for further analysis of the characteristics of the sediment. At the same time, the detachable pipe section can be processed into different pipe wall roughness and material replacement. The pipe section makes the experimental operation flexible and changeable;

(3)装置设置溶硫剂加注系统,可有效评价和研究不同类型溶硫剂对硫沉积物的清除效果;(3) The device is equipped with a sulfur-dissolving agent filling system, which can effectively evaluate and study the removal effect of different types of sulfur-dissolving agents on sulfur deposits;

(4)装置的管路系统设置防爆型电热带,可控制温度在指定值,当实验结束后,可以加热管壁,方便管壁附着的硫沉积物融化流走。(4) The pipeline system of the device is equipped with an explosion-proof electric heating belt, which can control the temperature at a specified value. When the experiment is over, the pipe wall can be heated, so that the sulfur deposits attached to the pipe wall can be melted and flowed away.

附图说明Description of drawings

图1为本发明整体结构示意图;Fig. 1 is the overall structure schematic diagram of the present invention;

图2为图1中高压气罐结构示意图;Fig. 2 is the structural representation of high pressure gas tank in Fig. 1;

图3为图1拆卸式管段结构示意图;Fig. 3 is a schematic diagram of the structure of the disassembled pipe section of Fig. 1;

图4为图3中A-A截面侧视图;Fig. 4 is A-A sectional side view in Fig. 3;

图5为图1中拆卸管段垂直取样过程结构示意图;Fig. 5 is the structural schematic diagram of the vertical sampling process of dismantling the pipe section in Fig. 1;

图6为图5中固定支架俯视图;Fig. 6 is the top view of the fixed bracket in Fig. 5;

图7为图1中溶硫剂加注系统结构示意图。FIG. 7 is a schematic structural diagram of the sulfur-dissolving agent filling system in FIG. 1 .

图中,1、高压气罐;2、第一控制阀门;3、第一压力表;4、压缩机;5、第二压力表;6、第二控制阀门;7、溶硫剂加注系统;8、控温水浴入口;9、拆卸式管段;10、控温水浴;11、水管;12、控温水浴出口;121、管路泄压阀;13、防爆电热带;14、第三控制阀门;141、旁通管路;15、第一止回阀;16、流量计;17、第二止回阀;18、第四控制阀门;19、第五控制阀门;20、高压气罐罐体;21、气体回流管线;22、电加热装置;23、废气废液外排管线;24、高压气罐控制阀门I;25、气体加注管线;26、高压气罐控制阀门II;27、气体流出管线;28、高压气罐压力表;29、安全泄压阀;30、夹套外层;31、夹套内层;32、拧紧螺母;33、拧紧螺杆;34、环道管线;35、为第一夹持固定环;36、第二夹持固定环;37、固定支架;38、融化的硫沉积物;39、烧杯;40、螺母;41、螺杆;42、溶硫剂储罐;43、液位计;44、储罐安全泄压阀;45、温度计;46、储罐压力表;47、泄流阀;48、泄流管线;49、储罐控制阀门;50、液体泵;51、储罐流量计;52、雾化器;53、溶硫剂加注口。In the figure, 1, high pressure gas tank; 2, first control valve; 3, first pressure gauge; 4, compressor; 5, second pressure gauge; 6, second control valve; 7, dissolved sulfur agent filling system ;8. Temperature-controlled water bath inlet; 9. Detachable pipe section; 10. Temperature-controlled water bath; 11. Water pipe; 12. Temperature-controlled water bath outlet; 121. Pipeline pressure relief valve; Valve; 141, bypass pipeline; 15, first check valve; 16, flow meter; 17, second check valve; 18, fourth control valve; 19, fifth control valve; 20, high pressure gas tank 21. Gas return pipeline; 22. Electric heating device; 23. Exhaust gas and waste liquid discharge pipeline; 24. High-pressure gas tank control valve I; 25. Gas filling pipeline; 26. High-pressure gas tank control valve II; 27. Gas outflow pipeline; 28. Pressure gauge of high-pressure gas tank; 29. Safety relief valve; 30. Outer layer of jacket; 31. Inner layer of jacket; 32. Tighten nut; 33. Tighten screw; 34. Ring pipeline; 35 , is the first clamping and fixing ring; 36, the second clamping and fixing ring; 37, the fixing bracket; 38, the molten sulfur deposit; 39, the beaker; 40, the nut; ;43, liquid level gauge; 44, storage tank safety relief valve; 45, thermometer; 46, storage tank pressure gauge; 47, relief valve; 48, relief pipeline; 49, storage tank control valve; 50, liquid pump ; 51, storage tank flowmeter; 52, atomizer; 53, the filling port of dissolved sulfur agent.

具体实施方式Detailed ways

下面结合附图和实施例对本发明进行详细描述。The present invention will be described in detail below with reference to the accompanying drawings and embodiments.

实施例Example

如图所示,一种含硫天然气管道硫沉积实验装置,包括储气系统、环道系统和溶硫剂加注系统,所述储气系统为高压气罐1,所述环道系统包括环道管线34,环道管线上连通高压气罐和拆卸式管段9,高压气罐的一侧和拆卸式管段之间依次设有第一控制阀门2、第一压力表3、压缩机4、第二压力表5和溶硫剂加注系统7,溶硫剂加注系统7和环道管线之间设有第二控制阀门6;所述拆卸式管段的两端分别设有控温水浴入口8和控温水浴出口12,控温水浴入口8和控温水浴出口12之间通过水管11连通控温水浴10;所述拆卸式管段9和高压气罐的另一侧之间依次设有第一止回阀15、质量流量计16、第二止回阀17和第五控制阀门19;环道管线34上在第一止回阀15和第二止回阀17的两端并联旁通管路141,旁通管路141和环道管线34之间分别设有第三控制阀门14和第四控制阀门18。As shown in the figure, an experimental device for sulfur deposition in a sulfur-containing natural gas pipeline includes a gas storage system, a ring channel system and a sulfur-dissolving agent filling system. The gas storage system is a high-pressure gas tank 1, and the ring channel system includes a ring channel system. The pipeline 34, the loop pipeline is connected with the high-pressure gas tank and the dismantling pipe section 9, and the first control valve 2, the first pressure gauge 3, the compressor 4, the first control valve 2, the first pressure gauge 3, the compressor 4, the first control valve 2, the first pressure gauge 3, the first Two pressure gauges 5 and sulfur-dissolving agent filling system 7, a second control valve 6 is provided between the sulfur-dissolving agent filling system 7 and the loop pipeline; And the temperature-controlling water bath outlet 12, the temperature-controlling water-bath inlet 8 and the temperature-controlling water-bath outlet 12 are connected to the temperature-controlling water bath 10 through the water pipe 11; Check valve 15 , mass flow meter 16 , second check valve 17 and fifth control valve 19 141, a third control valve 14 and a fourth control valve 18 are respectively provided between the bypass pipeline 141 and the loop pipeline 34.

所述高压气罐1为立式罐,高压气罐罐体20上分别连通有气体回流管线21、废气废液外排管线23、气体加注管线25和气体流出管线27,所述的废气废液外排管线23上设有高压气罐控制阀门I 24,所述的气体加注管线25上设有高压气罐控制阀门II26,所述的高压气罐罐体20的内部安装有电加热装置22,电加热装置22可采用陶瓷电加热圈,具有性能稳定、防腐、加热快、散热均匀、绝缘性能良好、耐高压等优点,所述的高压气罐罐体20的上部安装有高压气罐压力表28和安全泄压阀29。The high-pressure gas tank 1 is a vertical tank, and the high-pressure gas tank body 20 is respectively connected with a gas return line 21, a waste gas and waste liquid discharge line 23, a gas filling line 25 and a gas outflow line 27. The liquid discharge pipeline 23 is provided with a high-pressure gas tank control valve I 24, the described gas filling pipeline 25 is provided with a high-pressure gas tank control valve II 26, and an electric heating device is installed inside the described high-pressure gas tank body 20 22. The electric heating device 22 can use a ceramic electric heating ring, which has the advantages of stable performance, anti-corrosion, fast heating, uniform heat dissipation, good insulation performance, high pressure resistance, etc. The upper part of the high-pressure gas tank body 20 is installed with a high-pressure gas tank Pressure gauge 28 and safety relief valve 29.

所述高压罐罐体20由抗硫腐蚀材料制作,所述气体回流管线21是含硫天然气经过环道系统后循环回高压气罐的管路,所述电加热装置22具有防爆和控温功能,可以将高压储罐内的天然气加热至指定温度,所述废气废液外排管线23及高压气罐控制阀门I 24的目的是定期清理高压气罐内的残留气体和液体,所述气体加注管线25和高压气罐控制阀门II26用来控制加注含硫天然气至罐内,含硫天然气为现场取样的气体,使实验结果可以真实反映现场硫沉积情况,所述气体流出管线27的含硫天然气进入环道系统,所述高压气罐压力表28可以监测罐内气体的压力,所述安全泄压阀29可以起到过压保护作用。The high-pressure tank body 20 is made of sulfur-resistant corrosion-resistant materials, the gas return line 21 is a pipeline for the sulfur-containing natural gas to be circulated back to the high-pressure gas tank after passing through the loop system, and the electric heating device 22 has the functions of explosion-proof and temperature control. , the natural gas in the high-pressure storage tank can be heated to a specified temperature, the purpose of the waste gas and waste liquid discharge line 23 and the high-pressure gas tank control valve I 24 is to regularly clean up the residual gas and liquid in the high-pressure gas tank, and the gas added The injection line 25 and the high-pressure gas tank control valve II26 are used to control the injection of sulfur-containing natural gas into the tank. The sulfur-containing natural gas is the gas sampled on site, so that the experimental results can truly reflect the on-site sulfur deposition. Sulfur natural gas enters the loop system, the high-pressure gas tank pressure gauge 28 can monitor the gas pressure in the tank, and the safety relief valve 29 can play an overpressure protection role.

所述压缩机4可以根据实验条件需要,组装多个压缩机串联,实现多级增压。The compressor 4 can be assembled with multiple compressors in series according to the requirements of the experimental conditions to realize multi-stage supercharging.

所述拆卸式管段9与环道管线34通过法兰连接,拆卸式管段9由外层夹套30套装在内层夹套31的外部构成夹套结构,控温水浴入口8和控温水浴出口12与夹套内腔连通。The detachable pipe section 9 and the loop pipeline 34 are connected by flanges. The detachable pipe section 9 is set by the outer jacket 30 to form a jacket structure outside the inner jacket 31. The temperature-controlled water bath inlet 8 and the temperature-controlled water bath outlet are 12 communicates with the inner cavity of the jacket.

所述外层夹套30在同一剖面上下两个方向设置控温水浴入口8和控温水浴出口12,控温水浴入口8和控温水浴出口12分别连接控温水浴10,外层夹套30和内层夹套31之间的环形空间内供循环水流动,以此来控制实验管段的壁温。The outer jacket 30 is provided with a temperature-controlling water bath inlet 8 and a temperature-controlling water-bath outlet 12 in the upper and lower directions of the same section. The annular space between it and the inner jacket 31 is for circulating water to flow, so as to control the wall temperature of the experimental pipe section.

所述的法兰通过拧紧螺母32和拧紧螺杆33连接固定,拧紧螺母32、拧紧螺杆33和法兰盘之间设有密封垫片。The flange is connected and fixed by tightening the nut 32 and the tightening screw 33, and a sealing gasket is provided between the tightening nut 32, the tightening screw 33 and the flange.

所述的环道管线34上缠绕防爆电热带13,环道管线34上设有管路泄压阀121。The said loop pipeline 34 is wound with the explosion-proof electric tape 13, and the loop pipeline 34 is provided with a pipeline pressure relief valve 121.

所述防爆电热带13具有开关控制和加热指示灯部件,方便操作,防爆电热带13可以将管壁温度控制在指定值上。所述旁通管路141便于清理管线内的硫沉积物,保证融化的硫沉积物不流经流量计,减少对流量计的不利影响。所述流量计16为质量流量计,所述第一止回阀15和第二止回阀17设置在流量计16两侧,防止气体流向改变破坏流量计内部结构。The explosion-proof electric belt 13 has switch control and heating indicator light components, which is convenient for operation, and the explosion-proof electric belt 13 can control the temperature of the pipe wall to a specified value. The bypass pipeline 141 is convenient for cleaning the sulfur deposits in the pipeline, ensuring that the melted sulfur deposits do not flow through the flowmeter, and reducing the adverse effect on the flowmeter. The flowmeter 16 is a mass flowmeter, and the first check valve 15 and the second check valve 17 are arranged on both sides of the flowmeter 16 to prevent the change of the gas flow direction from damaging the internal structure of the flowmeter.

所述溶硫剂加注系统包括溶硫剂储罐42,所述溶硫剂储罐采用卧式结构,溶硫剂储罐上安装有液位计43、储罐安全泄压阀44、温度计45、储罐压力表46、泄流管线48、溶硫剂加注口3和液体泵50,泄流管线48上安装泄流阀47,液体泵50和溶硫剂储罐42之间安装储罐控制阀门49,液体泵50通过管道连接有雾化器52,液体泵50和雾化器52之间安装储罐流量计51,雾化器52通过第二控制阀门6与环道管线34连通。The sulfur-dissolving agent filling system includes a sulfur-dissolving agent storage tank 42, the sulfur-dissolving agent storage tank adopts a horizontal structure, and a liquid level gauge 43, a storage tank safety pressure relief valve 44, a thermometer are installed on the dissolving sulfur agent storage tank 45. Tank pressure gauge 46, drain line 48, sulfur-dissolving agent filling port 3 and liquid pump 50, a drain valve 47 is installed on the drain line 48, and a storage tank is installed between the liquid pump 50 and the sulfur-dissolving agent storage tank 42. The tank control valve 49, the liquid pump 50 is connected with the atomizer 52 through the pipeline, the storage tank flow meter 51 is installed between the liquid pump 50 and the atomizer 52, and the atomizer 52 is communicated with the loop pipeline 34 through the second control valve 6 .

溶硫剂储罐42采用抗腐蚀性材料制作,所述液位计43可以监测储罐内溶硫剂液位,所述储罐安全泄压阀44起到过压保护作用,所述温度计45可以监测储罐内溶硫剂温度,所述储罐压力表46可以读取储罐内压力,所述泄流阀47和泄流管线48可以排除储罐内残余液体,所述雾化器52可以将溶硫剂变为雾状喷入环道管线,使得溶硫剂与硫颗粒充分接触,增强溶硫效果,所述溶硫剂加注口53可以根据需要加注特定类型和剂量的溶硫剂。The sulfur-dissolving agent storage tank 42 is made of corrosion-resistant materials, the liquid level gauge 43 can monitor the liquid level of the sulfur-dissolving agent in the storage tank, the storage tank safety relief valve 44 plays an overpressure protection function, and the thermometer 45 The temperature of the dissolved sulfur agent in the storage tank can be monitored, the storage tank pressure gauge 46 can read the pressure in the storage tank, the drain valve 47 and the drain line 48 can remove the residual liquid in the storage tank, and the atomizer 52 The sulfur-dissolving agent can be changed into a mist and sprayed into the loop pipeline, so that the sulfur-dissolving agent can fully contact with the sulfur particles, and the effect of dissolving sulfur can be enhanced. Sulfur agent.

所述拆卸式管段9拆卸后由固定装置固定,所述固定装置包括夹持固定环及固定支架37,固定支架设置在夹持固定环的两侧,所述夹持固定环包括两个弧形的第一夹持固定环35和第二夹持固定环36,第一夹持固定环35和第二夹持固定环36的端部设有安装耳,安装耳上设置有螺纹孔,螺母和螺杆穿过螺纹孔将第一夹持固定环和第二夹持固定环固定连接,从而将拆卸式管段夹紧。The detachable pipe section 9 is fixed by a fixing device after being disassembled. The fixing device includes a clamping and fixing ring and a fixing bracket 37. The fixing brackets are arranged on both sides of the clamping and fixing ring, and the clamping and fixing ring includes two arcs. The first clamping and fixing ring 35 and the second clamping and fixing ring 36, the ends of the first clamping and fixing ring 35 and the second clamping and fixing ring 36 are provided with mounting ears, and the mounting ears are provided with threaded holes, nuts and The screw rod passes through the threaded hole to fixedly connect the first clamping and fixing ring and the second clamping and fixing ring, so as to clamp the detachable pipe section.

所述拆卸式管段固定好后,可以开启控温水浴,加热拆卸式管段,将管壁上沉积的硫沉积物全部融化至烧杯内,进行称重以及测试分析。由此,可以分析特定时间、温度、压力、流速等变量对硫沉积规律的影响,达到实验目的。After the detachable pipe section is fixed, a temperature-controlled water bath can be turned on, the detachable pipe section can be heated, and all the sulfur deposits deposited on the pipe wall are melted into the beaker for weighing and test analysis. In this way, the influence of variables such as specific time, temperature, pressure, flow rate, etc. on the sulfur deposition law can be analyzed to achieve the experimental purpose.

硫沉积规律实验研究时的操作过程如下:The operation process of the experimental study of sulfur deposition law is as follows:

将现场天然气管线内取得的高含硫天然气加入高压气罐1,开启电加热装置22将天然气加热到指定温度,调整第一控制阀门2和第五控制阀门19为开启状态,调整第二控制阀门6、管路泄压阀121、第三控制阀门14、第四控制阀门18、高压气罐控制阀门I24、高压气罐控制阀门II26为关闭状态,将控温水浴10开启,控制实验管段即拆卸式管段在指定温度上,开启第一止回阀15和第二止回阀17,启动压缩机4,使天然气在管路系统循环,通过控制压缩机功率以及阀门开度大小可以控制气体压力和流速,通过高压气罐的电加热装置可以控制气体进入实验管段的温度,通过控温水浴可以控制实验管段的管壁温度,由此实现对特定流速、气体温度、气体温度与管壁温差、压力等变量对硫沉积规律的研究。此外,可拆卸实验管段可以采用不同材质或者表面粗糙度的管壁加工,方便更换,由此可以研究表面粗糙度以及材质对硫沉积的影响规律。The high-sulfur natural gas obtained from the natural gas pipeline on site is added to the high-pressure gas tank 1, the electric heating device 22 is turned on to heat the natural gas to the specified temperature, the first control valve 2 and the fifth control valve 19 are adjusted to be open, and the second control valve is adjusted. 6. The pipeline pressure relief valve 121, the third control valve 14, the fourth control valve 18, the high-pressure gas tank control valve I24, and the high-pressure gas tank control valve II26 are closed, and the temperature-controlled water bath 10 is opened to control the experimental pipe section. At the specified temperature, the first check valve 15 and the second check valve 17 are opened, the compressor 4 is started, and the natural gas is circulated in the pipeline system. By controlling the compressor power and the valve opening, the gas pressure and The flow rate, the temperature of the gas entering the experimental pipe section can be controlled by the electric heating device of the high-pressure gas tank, and the pipe wall temperature of the experimental pipe section can be controlled by the temperature-controlled water bath, thereby realizing the specific flow rate, gas temperature, gas temperature and pipe wall temperature difference, pressure Equal variables to study the law of sulfur deposition. In addition, the detachable experimental pipe section can be processed with pipe walls of different materials or surface roughness, which is convenient for replacement, so that the influence of surface roughness and material on sulfur deposition can be studied.

硫沉积实验结束后,关闭第一控制阀门2和第五控制阀门19,关闭压缩机,同时开启管路泄压阀121将管路内残存的气体排入特定装置内,进行无害化处理,将可拆卸实验管段与环道系统管线分离,将实验管段垂直放置夹紧,开启控温水浴10,并加热实验管段,将管壁上沉积的硫沉积物38全部融化至烧杯39内,进行称重以及测试分析。由此,可以分析特定时间、温度、压力、流速等变量对硫沉积规律的影响,达到实验目的。After the sulfur deposition experiment, close the first control valve 2 and the fifth control valve 19, close the compressor, and open the pipeline pressure relief valve 121 at the same time to discharge the gas remaining in the pipeline into a specific device for harmless treatment, Separate the detachable experimental pipe section from the loop system pipeline, place the experimental pipe section vertically and clamp it, turn on the temperature-controlled water bath 10, and heat the experimental pipe section, melt all the sulfur deposits 38 deposited on the pipe wall into the beaker 39, and weigh. weight and test analysis. In this way, the influence of variables such as specific time, temperature, pressure, flow rate, etc. on the sulfur deposition law can be analyzed to achieve the experimental purpose.

溶硫剂溶硫效果实验研究时的操作过程如下:The operation process of the experimental study on the effect of the dissolved sulfur solvent is as follows:

如要研究溶硫剂对管壁上硫沉积物的清除效果,首先进行一定时间特定条件的硫沉积实验,而后对实验管段内的硫沉积物进行称重,称重时对整个实验管段进行称重,减去无沉积物时的管段质量即得到管壁上附着的沉积物的质量,而后重新将实验管段连接到环道系统上,保证泄流阀47关闭,开启储罐控制阀门49和第一控制阀门6,开启液体泵50,开启雾化器52。同时,再次开启环道系统,使得高含硫气体在管路内继续循环,并带动雾化后的溶硫剂在管路系统内共同流动,经过特定时间后,可以关闭环道系统和溶硫剂加注系统,再次取下实验管段对沉积物进行称重,经过对比,可以得出不同类型溶硫剂对硫沉积物的溶硫效果,进而对比优选。To study the effect of dissolving sulfur agent on the removal of sulfur deposits on the pipe wall, first carry out a sulfur deposition experiment under specific conditions for a certain period of time, and then weigh the sulfur deposits in the experimental pipe section, and weigh the entire experimental pipe section during weighing. The mass of the sediment attached to the pipe wall is obtained by subtracting the mass of the pipe section when there is no sediment, and then the experimental pipe section is reconnected to the loop system to ensure that the relief valve 47 is closed, and the storage tank control valve 49 and No. 4 are opened. A control valve 6 turns on the liquid pump 50 and turns on the atomizer 52. At the same time, open the loop system again, so that the high-sulfur gas continues to circulate in the pipeline, and drive the atomized dissolved sulfur agent to flow together in the pipeline system. After a certain time, the loop system and the dissolved sulfur can be closed. The agent filling system was used, and the experimental pipe section was removed again to weigh the sediment. After comparison, the sulfur-dissolving effect of different types of sulfur-dissolving agents on the sulfur sediment can be obtained, and then the comparison and optimization can be made.

Claims (3)

1. A sulfur deposition experimental device for a sulfur-containing natural gas pipeline is characterized by comprising a gas storage system, an annular system and a sulfur dissolving agent filling system, wherein the gas storage system is a high-pressure gas tank (1), the annular system comprises an annular pipeline (34), the annular pipeline is communicated with the high-pressure gas tank and a detachable pipeline section (9), a first control valve (2), a first pressure gauge (3), a compressor (4), a second pressure gauge (5) and a sulfur dissolving agent filling system (7) are sequentially arranged between one side of the high-pressure gas tank and the detachable pipeline section, and a second control valve (6) is arranged between the sulfur dissolving agent filling system (7) and the annular pipeline; two ends of the detachable pipe section are respectively provided with a temperature-controlled water bath inlet (8) and a temperature-controlled water bath outlet (12), and the temperature-controlled water bath inlet (8) and the temperature-controlled water bath outlet (12) are communicated with a temperature-controlled water bath (10) through a water pipe (11); a first check valve (15), a mass flow meter (16), a second check valve (17) and a fifth control valve (19) are sequentially arranged between the detachable pipe section (9) and the other side of the high-pressure gas tank; a bypass pipeline (141) is connected in parallel at two ends of the first check valve (15) and the second check valve (17) on the loop pipeline (34), and a third control valve (14) and a fourth control valve (18) are respectively arranged between the bypass pipeline (141) and the loop pipeline (34);
at least one compressor (4) is arranged, and a plurality of compressors are installed in series;
the detachable pipe section (9) is connected with the loop pipeline (34) through a flange, the detachable pipe section (9) is sleeved outside the inner jacket (31) through the outer jacket (30) to form a jacket structure, and the temperature-controlled water bath inlet (8) and the temperature-controlled water bath outlet (12) are communicated with the inner cavity of the jacket;
an explosion-proof electric heating belt (13) is wound on the loop pipeline (34), and a pipeline pressure release valve (121) is arranged on the loop pipeline (34);
the sulfur dissolving agent filling system comprises a sulfur dissolving agent storage tank (42), the sulfur dissolving agent storage tank is of a horizontal structure, a liquid level meter (43), a storage tank safety pressure relief valve (44), a thermometer (45), a storage tank pressure gauge (46), a drainage pipeline (48), a sulfur dissolving agent filling port (3) and a liquid pump (50) are mounted on the sulfur dissolving agent storage tank, a drainage valve (47) is mounted on the drainage pipeline (48), a storage tank control valve (49) is mounted between the liquid pump (50) and the sulfur dissolving agent storage tank (42), the liquid pump (50) is connected with an atomizer (52) through a pipeline, a storage tank flowmeter (51) is mounted between the liquid pump (50) and the atomizer (52), and the atomizer (52) is communicated with a loop pipeline (34) through a second control valve (6);
the utility model discloses a detachable pipe section, including dismantlement formula pipe section (9), dismantlement formula pipe section is fixed by fixing device after dismantling, fixing device includes that the solid fixed ring of centre gripping and fixed bolster (37), and the fixed bolster sets up the both sides at the solid fixed ring of centre gripping, the solid fixed ring of centre gripping includes solid fixed ring (35) of two curved first centre gripping and solid fixed ring (36) of second centre gripping, and the tip of the solid fixed ring of first centre gripping (35) and the solid fixed ring of second centre gripping (36) is equipped with the installation ear, is provided with the screw hole on the installation ear, and nut and screw rod pass the screw hole with the solid fixed ring fixed connection of the.
2. The sulfur deposition experiment device for the sulfur-containing natural gas pipeline as claimed in claim 1, wherein the high-pressure gas tank (1) is a vertical tank, the high-pressure gas tank body (20) is respectively communicated with a gas return line (21), a waste gas and liquid discharge line (23), a gas filling line (25) and a gas outflow line (27), the waste gas and liquid discharge line (23) is provided with a high-pressure gas tank control valve I (24), the gas filling line (25) is provided with a high-pressure gas tank control valve II (26), the high-pressure gas tank body (20) is internally provided with an electric heating device (22), and the upper portion of the high-pressure gas tank body (20) is provided with a high-pressure gas tank pressure gauge (28) and a safety relief valve (29).
3. The experimental device for sulfur deposition in the sulfur-containing natural gas pipeline as claimed in claim 1, wherein the flange is fixedly connected with the tightening nut (32) and the tightening screw (33), and sealing gaskets are arranged between the tightening nut (32), the tightening screw (33) and the flange.
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Publication number Priority date Publication date Assignee Title
CN110553958B (en) * 2019-09-04 2022-07-01 辽宁石油化工大学 Submarine mixed transportation pipeline wax deposition simulation experiment device and operation method thereof
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CN112014261B (en) * 2020-09-04 2022-04-26 西南石油大学 A device and method for measuring adsorbed sulfur content based on the principle of solvent dissolution
CN112945812B (en) * 2021-01-31 2022-06-07 西南石油大学 Sulfur deposition testing device for sulfur-containing natural gas gathering and transportation pipeline

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3223156A (en) * 1962-04-06 1965-12-14 Gewerkschaft Elwerath Method for the prevention of sulfur deposit in the riser pipes in the extraction of natural gases laden with hydrogen sulfide when elementary sulfur is present in the deposit
US3331657A (en) * 1962-04-06 1967-07-18 Gewerkschaft Elwerath Method of preventing the depositing of sulfur in the riser pipes in producing natural gases laden with hydrogen sulfide and containing elemental sulfur in solution
US3796265A (en) * 1972-06-07 1974-03-12 J Eickmeier Method for producing high hydrogen sulfide content gas wells
JP2015218602A (en) * 2014-05-14 2015-12-07 トヨタ自動車株式会社 Exhaust gas purification system for internal combustion engine
CN206557197U (en) * 2017-03-21 2017-10-13 中国石油大学(华东) It is a kind of to be used for the experimental provision of gas hydrate study in deep water hydrocarbon gathering line
CN206671302U (en) * 2017-04-24 2017-11-24 中国石油大学(北京) Crude oil pipeline wax deposit analogue means integrated with pigging
CN208076339U (en) * 2018-03-26 2018-11-09 中国石油大学(华东) A kind of experiment circuit device of waxy crude oil wax deposit test
CN109060616A (en) * 2018-07-23 2018-12-21 西南石油大学 A kind of high-precision sulphur deposition in wellhole influence factor visual testing device and method
CN109668824A (en) * 2019-01-22 2019-04-23 北京科技大学 Simulate the high speed humidity corrosion loop experimental provision of natural gas line internal corrosion environment

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3223156A (en) * 1962-04-06 1965-12-14 Gewerkschaft Elwerath Method for the prevention of sulfur deposit in the riser pipes in the extraction of natural gases laden with hydrogen sulfide when elementary sulfur is present in the deposit
US3331657A (en) * 1962-04-06 1967-07-18 Gewerkschaft Elwerath Method of preventing the depositing of sulfur in the riser pipes in producing natural gases laden with hydrogen sulfide and containing elemental sulfur in solution
US3796265A (en) * 1972-06-07 1974-03-12 J Eickmeier Method for producing high hydrogen sulfide content gas wells
JP2015218602A (en) * 2014-05-14 2015-12-07 トヨタ自動車株式会社 Exhaust gas purification system for internal combustion engine
CN206557197U (en) * 2017-03-21 2017-10-13 中国石油大学(华东) It is a kind of to be used for the experimental provision of gas hydrate study in deep water hydrocarbon gathering line
CN206671302U (en) * 2017-04-24 2017-11-24 中国石油大学(北京) Crude oil pipeline wax deposit analogue means integrated with pigging
CN208076339U (en) * 2018-03-26 2018-11-09 中国石油大学(华东) A kind of experiment circuit device of waxy crude oil wax deposit test
CN109060616A (en) * 2018-07-23 2018-12-21 西南石油大学 A kind of high-precision sulphur deposition in wellhole influence factor visual testing device and method
CN109668824A (en) * 2019-01-22 2019-04-23 北京科技大学 Simulate the high speed humidity corrosion loop experimental provision of natural gas line internal corrosion environment

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
超深高含硫气藏气—液硫两相渗流实验;顾少华 等;《天然气工业》;20181031;第70-75页 *
高含硫天然气输送管道内硫沉积研究进展;李长俊 等;《科学通报》;20180331;第63卷(第9期);第816-827页 *

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